|Publication number||US3730959 A|
|Publication date||May 1, 1973|
|Filing date||Jul 8, 1971|
|Priority date||Jul 8, 1971|
|Publication number||US 3730959 A, US 3730959A, US-A-3730959, US3730959 A, US3730959A|
|Inventors||C Horres, R Leonard|
|Original Assignee||Us Interior|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (7), Non-Patent Citations (1), Referenced by (52), Classifications (13)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Hori'es, Jr. et a1.
SUBSTlTUTE r012 MISSING XR s ATIcIIRooI/I III 0,730,959 [[451 ,May 1 1973 FABRICATION OF HIGH PRESSURE 2,757,439 8/1956 Burns .....264/3l7UX SEALS FOR WATER EQUILIBRATED 7 3,522,339 7/1970 Te Velde. ..264/261 X I FIBER BUNDLES I 1,082,231 12/1913 Nale ..264/26l X T Inventors: Charles Russell norm, In, Chapel OTHER PUBLICATIONS I i ggg Leonard Ralggh'l National I Academy of Sciences-National Research 0 0 I Council. Desalination Research Conference.  Assignecz The United States 01 America as Proceedings of the Conference on Desalination represented by the Secretary 01 the Research-Woods Hole, Mass, 14 June to 14 July Interior. I r I l96l.Hollow Fibers As Membranes for Reverse Osmosis" by Henry 1. Mahon, publication 942. 1963, pp; [-2] Filed. July 8,1971 345 348I I I I  Appl. No.: 160,668 Primary Examiner-Philip' E. Anderson 52 us. c1. ..264/263, 210/321, 264/265,
1 264/271, 264/317, 26 4/D1G. 44 Y 51 1m. (:1 ....B29d 3/02, B29d 27/00 [571 ABSTRACT  Field Of Search; ..264/41, 49, 221, The formation of high pressure seals for .water 1 6 4 l equilibrated, hollow fiber membranes is effected by in- 210/321 jecting a solution of gelatin around the active membrane area, chilling the solution to solidify the gelatin 1 I 'Ikeffl'ences Cited and immobilize the water, washing the ends or inactive area of the membrane with warm water, drying I UNITED STATES PATENTS the ends, and casting aseal on the solidified gelatin 3,422,008 1/1969 McLain ,J. ..2'10/22 surface. The gelatin is removed by heating and wash- 3 7()4.223 11/1972 Dietzsch et a1. ....210/321 X ing the fibers.
.551 3 1 12/1970 Cescon et a1. ..264/4l X 2,694,228 11/1954. Mathis ..264/317 X 12 Claims, 3Drawing Figures I II llI'I'I SURROUND FIBER \IVITH GELATIN SOLUTION I I I I SYEP 4 i g f t .T CAST,PLUS a ry ab CURE SEALANT Pate-mama, 1, 1973; f R 3,730,959
I I :2 Sha na- Shut 1 i .-.s.'-f." ti'fxrm R I I I l A :11! Va R was" auo onv nun suns STEP l,
SURROUND FIBER WiTH 575p 2 GELATIN SOLUTION CHILLHGELATIN F/GJ 2 v 7 STEP 5 STEP '4 REMOVE GELATIN CAST,PLUS CURE, SEALANT INVENTORS CHARLES RUSSELLHORRES RICHARD 1., LEONARD ATTORNEY l FABRICATION or area PRESSURE SEALS FOR I WATER EQUILIBRATED FIBER nunnws BACKGROUND,
One of the mostpromising techniques for the commercial desalination of saline waters, reverse osmosis is, as its name implies, the opposite of another process. Osmosis is a naturally occurring phenomenon in which solvent from a d lute Solu on pa r g H) tion ofseals in other systems with similar problems.
The usual methodof forming the seals on the end of a hollow fiber membrane bundle'is shown, for example,
brane into a more concentrated solution. This flow will continue unless opposed by a pressure equal in force to the" characteristic osmotic, pressure of the system. ln reverse osmosis, therefore, the flow of solvent is completely reversed by applying a pressure greater .than osmotic to the concentrated solution. Thus, by
contacting an appropriatemembrance with saline water under sufficient pressure, 'pure water will be forced through the membrane and recovered on the opposite side.
Obviously, the key to this process is in finding a membrane which demonstrates normal osmosis with respect to the solution to be separated. Thus, reverse osmosis was not known as amethod for desalinating aqueous sodium chloride solutions until late in the 1950's when itwas discovered that cellulose acetate allowed the passage of water from a dilute solution to a more concentrated one while prohibiting the flow of salt. Since that time new methodsof forming cellulose acetate membranes and new membrane materials have been discovered in an attempt to find a commercially acceptable membrane.
To be economical a reverse osmosis membrane must meet the requirements of adequate selectivity and water flux. Selectivity refers to the relative ability of the membrane to permit the flow of solvent while rejecting the passage of salt. The ideal membrane would v completely prohibit the flowof salt. Naturally, even with a membrane of perfect selectivity, the process will not be economical if pure water merely trickles through it. The second requirement of adequate flux,
. therefore, refers to the quantity of pure water flowing through a unit area of the membrane in a certain leaks in the system, membrane seals separating the high pressure areas from thecollection zones are critical in all reverse osmosis-desalination systems. The formation of seals around the'ends of the many little fibers used in a a hollow fiber bundle has created special problems. It is in U.S."Pat. No. 3,442,389 to M cLain. A mold is placed around the ends of the hollow fibers and a solidifiable material such as epoxy resin is poured around these ends. After the resin hardens, a cross sectional cut may amount of time. Research to date has been effective in.
economic savings. Some of the most promising-com-- mercial systems use bundles of-membranes formed into tiny hollow fibers, typically with outside diameters of from 50 to 40 microns and with wall thickness to tliamctcr ratios of from ().l5 to 0.35. These fibers resent a tremendously large membrane surface area er volume of equipment and thus, even if the flux or flow per area of the membrane is not the best, the rate of recovery of pure water from the system may be least be acceptable. Although desalination systems using bundles of'hollow fibers may actually be used in many specific different designs, the usual one will have the saline water pressurized from about l5 to L500 psi or more on the outside of the hollow fibers. Pure water moves through the membrane surfaces and is channeled by the fibers to collection means outside the desalination area.
be partially or completely. impaired. Most membrane be made through the resin and mold to expose the fiber ends. I
As mentioned in the patent, in order to form an ef fective seal it is necessary to use a sealant which is fluid enough to completely surround and encapture all the fiber 'ends in the closely packed bundle. The patent, however, acknowledges that if the sealant is very fluid, there is a tendency for wicking" to occur. In this phenomenon sealant creeps along the'fibers particu larly in channels formed between parallel fibers and out onto the active portions of the membrane. Activeportion" refers to that partof the membranefiber through' which reverse osmosis and, desalination is effected as opposed to the inactive'portions around which the seal isformed and which extend beyond the seal to the product collection means. Unfortunately, sealant which wicks onto the active surfaces hardens there and deadens these active areas. 7
US. Pat. No. 3,442,002 to Geary et al'. shows one solution to'the problem o fwicking centrifugal casting of'the seal. By rotating the fiber bundle during casting and curing of the membrane a centrifugal force is applied outwardly away from the active areas thereby offsetting the forces which cause wicking to occur.
Although the method of Geary et almay be effective in preventing wicking and localized deadening of active membrane surfaces, the membrane surfaces may still materials are water equilibrated and from the time of theirformation to their use they are kept in contact with water; this is particularly true of membranes of celluloseacetate and other cellulose derivatives. However, a problem exists since a satisfactory sealant for high pressure use has not been found for wet fibers. Either the moisture in and on the fiber is not compatible with the sealant, terminating cure, or the bond formed is not strong enough to prevent separation from the fiber as it'drie's during curing. Attempts to form seals while drying only the ends of the fibers have failed because water wicks from the other membrane areas Because of the high pressures employed and the contamination of product water which might be caused by into the seal. Unfortunately, allowing the membranes to be driedand to remain'dryingduring casting and these problems and it'is an objectof our invention to improve the niethodof forming seals on the end of hollow fiber waterequilibrated'revrse osmosis membranes. v
More generally, it is an object of our invention to improve the method of forming seals where the wicking" of sealant from the area being sealed or the wicking of liquids into the seal may present problems.
It is also a general object of our invention to improve the method of forming seals whenever the areas outside the seal are water equilibrated.
The basic steps of our process will be described in the following specification and are illustrated in FIG. 1 showing the formation of a seal on a hollow fiber bundle.
FIG. 2 illustrates a typical hollow fiber bundle and seal formed by the process and suitable for use in the reverse osmosis desalination apparatus shown in FIG. 3.
INVENTION We have now found a method for avoiding the previous disadvantages of forming seals for water equilibrated hollow fiber membranes. The essence of the invention is that a distinct separation is formed between dry and wet fiber regions so that the properties of the active membrane areas are not impaired when the inactive membrane regions are dried for seal formation. This result is achieved by surrounding the active fiber areas with a water immobilizing gel and thereafter forming the seal on the dry inactive fiber region.
This process is illustrated in FIG. 1. A bundle of looped membrane fibers 1 are placed in an appropriate container such as a tube or cylinder 3 such that all the.
fiber ends 2 are exposed. A warm aqueous solution of 4 gelatin or other water immobilizing material 4 is then poured into the container to surround the active membrane surfaces. Thus, the container is filled to a level such that all membrane surfaces that will be in contact with saline solution when the membranes are in operation will be covered by gelatin.
In step 2 the aqueous gelatin solution is chilled to solidify the gelatin 4 and immobilize the water surrounding the active membrane area. This may be accomplished, for example, by immersing the container 3 in an ice bath 5 at least up to the level of the solution in v the container. The gel solution is continuously chilled and kept in a solid state until after the seal has been cast and has cured.
Following the solidification 0f the aqueous gelatin solution, the fiber ends 2 are prepared for sealing. This preparation will most likely consist of washing the ends with warm water to remove any gelatin solution which has wickcd into these ends and then drying them for a sufficient time to insure that the casting and curing of the seal will not be impaired by retained water. The drying may be accomplished with either air or some inert atmosphere such as nitrogen, carbon dioxide or other gaseous media. While it is essential that the membrane ends are thoroughly dried before casting of the seal, extreme drying conditions should be avoided to prevent the ends from becoming brittle.
In step 4 the seal around the fiber ends is prepared. This may be accomplished, for example, by surrounding the fiber ends with a cylindrical mold 7, which is pressed into the surface of the gelatin. Subsequently, an epoxy resin or other suitable sealant is poured into the mold onto the solidified gelatin surface so that each fiber end is encaptured in resin. Any suitable epoxy resin or. other sealant'known in the art may be used such as those shown in U. S. Pat. No. 3,422,008 herein incorporated by reference. The fiber ends 2 extend beyond the sealant.
When this sealant has hardened, the solidified gelatin is removed from around the active membrane surfaces. This may be accomplished by warming the gelatin, removing the gelatin and fibers from the container, and washing the fibers to remove adhered traces of gelatin.
The membrane is then ready for use although it may be stored with at least the active membrane areas immersed in water. The hollow fiber bundle and attached seal 8 of hardened epoxy resin is shown in its finished form in step 5.
FIGS. 2 and 3 show how a hollow fiber membrane bundle and attached seal formed by our process could be used to desalinize water by reverse osmosis. The apparatus consists of a hollow tube 100 to which T joints I01 and 102 are attached at either end.
The membrane element 111 consists of hollow fiber membrane bundle 108 which is looped around the top of a support rod 107 such that all ends 110 of the fibers are held by a seal at the base of the support rod. The seal 109 consists of a length of stainless steel tubing in which the fibers are sealed with epoxy. The sealing is accomplished as previously discussed with the exception that the support rod is also included.
The membrane element is then positioned inside tube 100 as shown in the partial section of FIG. 3 and is held in place in T-joint 1 02 by pressure fitting 112 through which fiber ends 110 project.
In operation saline water under a pressure greater than osmotic is pumped into the tube through fitting 103. In tube 100 the saline water is purified by reverse osmosis-the membrane material selectively allowing water to pass through and enter the hollow fibers while excluding salt. Product water is then recovered as it drains from the ends 110 of the hollow fibers. Brine, more concentrated in salt than the feed saline water, leaves the tube by fitting 104. The final pressure fitting 1-05 opens to pressure gauge 106 by which the process can be monitored.
The apparatus used in FIG. 3 is merely illustrative of one system utilizing reverse osmosis membranes and the seals formed by our invention. It is apparent that the actual design of the membrane system could take many forms.
We expect that our invention can be used advantageously to form seals in systems with similar problems. For example, where a water equilibrated membrane is in a configuration where wicking is not a problem (ex. a single large diameter tube), it may still be desirable to surround the active membrane area with a water immobilizing gel during casting to protect these surfaces from the effects of drying. Similarly,
, wicking may be a problem in some situations in which hrane with a solidifiable materialand then casting the seal on the solidified material. While we have used a solution of gelatin as this solidifiable material, we also expect that other materialssu'ch aspolyglycols, agar solutions, or solutions of sodium silicates, commonly referred 'toas water glass could be used.
Finally, the reverse osmosis membranes which may be sealed by our process should not be limited to those which may be used for desalination, but include others suitable for usein the separation of water from electrolyte solutions including sea water, brackish water,
acid mine water, and industrial brines and bittems; the
About 10 inches of fiber remained exposed at the other end. A warm aqueous gelatin solution (2.8 wt. percent) drying the exposed end of said fiber, and casting a solidifiable sealant resin upon said water immobilizing gel so as to completely surround and 'encapture the dry inactive portion of said fiber membrane. I '2.--The process of claim 1 equlibrated hollow fiber is a reverse osmosis membrane.
. 3. The process of claim 1 wherein said water immobili'zing gel is solidified gelatin solution.
4. The process of claim 1 wherein said solidifiable sealant is epoxy resin.
5. The' process of claim l'wherein said water equlibrated hollow fiber membrane is.a plurality of water equlibrated-hollow fiber membranes.
6. The process of claim 5 wherein said plurality of Y water equlibrated-hollow fibermembranes are reverse was pumped into the pipe and then chilled to solidify the gelatin. The exposed fiber ends were washed with hot water to remove traces of gelatin which wicked before solidifying, and the fiber ends were'then dried in warm air while continuing to chill the gelatin. Finally, an epoxy sealant was cast onto the hardened gelatin layer with the seal mold surrounding the pipe. Afterthe' seal cured. the threaded fitting was detached and the I. In a process for the manufacture of a high pressure 7 seal molded around a water equilibrated hollow fiber osmosis membranes.
7. The processfof claim 6 wherein said plurality of 'water equlibrated hollow fiber membranes are reverse osmosis membranessuitable for use in water desalination. i
"8. A process for the formation of a high pressure seal around theend of a water-equlibrated hollow fiber membrane comprising:
surrounding the active area of said fiber with an aqueous solution of gelatin,
chilling said solution to solidify said gelatin,
washing the-exposed end of said fiber to remove any gelatin or aqueous solution,
drying said exposed end of said hollow fiber,
casting a solidifiable sealant resin around said end of said fiber nd adjacent said solidified gelatin solui curingsaid solidifiable sealant and a removing said solidified gelatin solution from around 7 said active fiber area. 9. The process of claim 8 wherein said water equlibrated hollow fiber is a reverse osmosis. membrane.
10. The process of claim 8 wherein said resin is epoxy resin.
ll. The process of claim 8 wherein said water equlibrated hollow fiber membrane is a plurality of water equlibrated hollow fiber membranes.
12. The process of claim 11 wherein said plurality of water equlibrated hollow fibers are reverse osmosis membranes, suitable for use in water desalination.
wherein said water
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US1082231 *||Mar 26, 1913||Dec 23, 1913||E J Hudnall||Method of setting tiles, bricks, and mosaics.|
|US2694228 *||May 16, 1950||Nov 16, 1954||Clark A Mathis||Method of making display assemblies|
|US2757439 *||Feb 25, 1955||Aug 7, 1956||Raytheon Mfg Co||Transistor assemblies|
|US3422008 *||Oct 24, 1963||Jan 14, 1969||Dow Chemical Co||Wound hollow fiber permeability apparatus and process of making the same|
|US3522339 *||Aug 1, 1966||Jul 28, 1970||Philips Corp||Method of making electrical monograin layer|
|US3551331 *||Sep 22, 1969||Dec 29, 1970||Du Pont||Reverse osmosis separations using a treated polyamide membrane|
|US3704223 *||Jun 6, 1969||Nov 28, 1972||Dietzsch Hans Joachim||Dialysis apparatus with capillary exchanger|
|1||*||National Academy of Sciences National Research Council. Desalination Research Conference. Proceedings of the Conference on Desalination Research. Woods Hole, Mass., 14 June to 14 July 1961. Hollow Fibers As Membranes for Reverse Osmosis by Henry I. Mahon, publication 942. 1963, pp. 345 348.|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3884814 *||Jul 23, 1973||May 20, 1975||Rhone Poulenc Sa||Apparatus for fractionating fluids|
|US3961010 *||Jun 28, 1973||Jun 1, 1976||Serck Industries Limited||Method of manufacturing heat exchangers|
|US3962766 *||May 31, 1974||Jun 15, 1976||Pont-A-Mousson S.A.||Process for assembling tubes of plastics material and assemblies resulting from said process|
|US3987142 *||Sep 27, 1974||Oct 19, 1976||Lewis Woolf Griptight Limited||Method of molding baby soother|
|US4038190 *||May 29, 1974||Jul 26, 1977||Rhone-Poulenc S.A.||Fluid fractionation apparatus and method of manufacturing the same|
|US4049765 *||Apr 26, 1976||Sep 20, 1977||Nippon Zeon Co., Ltd.||Method for setting end portion of bundle of thread-like bodies|
|US4061522 *||Feb 3, 1977||Dec 6, 1977||International Telephone And Telegraph Corporation||Method and apparatus for terminating a fiber optic bundle|
|US4098852 *||May 1, 1975||Jul 4, 1978||Rhone-Poulenc, S.A.||Process for carring out a gas/liquid heat-exchange|
|US4105731 *||Jul 1, 1977||Aug 8, 1978||Nippon Zeon Co., Ltd.||Method of embedding an end of a bundle of thread-like bodies in a molding material and controlling capillary action by said material|
|US4138460 *||Jun 10, 1977||Feb 6, 1979||Cordis Dow Corp.||Method for forming tubesheets on hollow fiber tows and forming hollow fiber bundle assemblies containing same|
|US4252765 *||Jan 16, 1980||Feb 24, 1981||Brumfield Robert C||Method for fabricating wound hollow fiber dialysis cartridges|
|US4568366 *||Aug 30, 1983||Feb 4, 1986||Baxter Laboratories, Inc.||In-line filter|
|US6592759||May 3, 2001||Jul 15, 2003||Zenon Environmental Inc.||Gel potting method and method to reduce twinning for filtering hollow fiber membranes|
|US6685832||Jun 13, 2002||Feb 3, 2004||Zenon Environmental Inc.||Method of potting hollow fiber membranes|
|US6964741||Mar 3, 2003||Nov 15, 2005||Zenon Environmental Inc.||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes|
|US7022231||Jan 30, 2004||Apr 4, 2006||Zenon Environmental Inc.||Apparatus incorporating potted hollow fiber membranes|
|US7063788||Feb 26, 2003||Jun 20, 2006||Zenon Environmental Inc.||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US7087173||May 10, 2004||Aug 8, 2006||Zenon Environmental Inc.||Inverted cavity aerator for membrane module|
|US7534353||Sep 19, 2006||May 19, 2009||Zenon Technology Partnership||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US7537701||Dec 17, 2007||May 26, 2009||Zenon Technology Partnership||Membrane filtration module with adjustable header spacing|
|US7615157||Feb 17, 2005||Nov 10, 2009||Zenon Technology Partnership||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US7708888||Sep 19, 2006||May 4, 2010||Zenon Technology Partnership||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US8075776||Feb 4, 2005||Dec 13, 2011||Zenon Technology Partnership||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US8133344||Jul 5, 2007||Mar 13, 2012||Asahi Kasei Chemicals Corporation||Process for production of hollow-fiber membrane bundles|
|US8852438||Mar 7, 2006||Oct 7, 2014||Zenon Technology Partnership||Membrane filtration module with adjustable header spacing|
|US20030164332 *||Mar 3, 2003||Sep 4, 2003||Mailvaganam Mahendran||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20030173706 *||Mar 17, 2003||Sep 18, 2003||Hamid Rabie||Gel potting method and method to reduce twinning for filtering hollow fibre membranes|
|US20040035780 *||Feb 26, 2003||Feb 26, 2004||Mailvaganam Mahendran||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20040118767 *||Sep 15, 2003||Jun 24, 2004||Henry Behmann||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20040182771 *||Jan 30, 2004||Sep 23, 2004||Mailvaganam Mahendran||Method of potting hollow fiber membranes|
|US20040238432 *||Jun 14, 2004||Dec 2, 2004||Mailvaganam Mahendran||Membrane filtration module with adjustable header spacing|
|US20050006308 *||May 10, 2004||Jan 13, 2005||Cote Pierre Lucien||Inverted cavity aerator for membrane module|
|US20050161384 *||Feb 4, 2005||Jul 28, 2005||Mailvaganam Mahendran||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20050173342 *||Apr 11, 2005||Aug 11, 2005||Pedersen Steven K.||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20050178728 *||Feb 17, 2005||Aug 18, 2005||Henry Behmann||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20050184002 *||Jan 6, 2005||Aug 25, 2005||Pedersen Steven K.||Method of potting hollow fiber membranes|
|US20060175243 *||Mar 7, 2006||Aug 10, 2006||Mailvaganam Mahendran||Membrane filtration module with adjustable header spacing|
|US20070007206 *||Sep 19, 2006||Jan 11, 2007||Henry Behmann||Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes|
|US20080093299 *||Dec 17, 2007||Apr 24, 2008||Mailvaganam Mahendran||Membrane filtration module with adjustable header spacing|
|US20100000939 *||Jul 5, 2007||Jan 7, 2010||Yuzuru Ishibashi||Process for production of hollow-fiber membrane bundles|
|US20100326897 *||Sep 10, 2010||Dec 30, 2010||Mailvaganam Mahendran||Membrane filtration module with adjustable header spacing|
|USRE39294||Oct 11, 2001||Sep 19, 2006||Zenon Environmental Inc.||Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate|
|USRE42669||Sep 6, 2011||Zenon Technology Partnership||Vertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces|
|EP0044075A1 *||Jul 14, 1981||Jan 20, 1982||Toyo Boseki Kabushiki Kaisha||Fluid separation element|
|EP0163900A2 *||Apr 23, 1985||Dec 11, 1985||Mitsubishi Rayon Co., Ltd.||Hollow-fiber filter module|
|EP0207379A1 *||Jun 19, 1986||Jan 7, 1987||Mitsubishi Rayon Co., Ltd.||Hollow-fiber filter module and filtration method using the same|
|EP1213048A1||Aug 8, 1996||Jun 12, 2002||Zenon Environmental Inc.||Method of potting fiber membranes|
|EP2042228A1 *||Jul 5, 2007||Apr 1, 2009||Asahi Kasei Chemicals Corporation||Process for produciton of hollow-fiber membrane bundles|
|EP2101843B1 *||Jan 10, 2008||Apr 13, 2016||3M Innovative Properties Company of 3M Center||Device for removing leukocytes from blood|
|WO2001085315A1 *||May 2, 2001||Nov 15, 2001||Zenon Environmental Inc.||Gel potting method for producing filtering hollow fibre membranes|
|WO2003086591A1 *||Apr 16, 2003||Oct 23, 2003||Puron Ag||Method for the production of a header comprising a fiber bundle made of open-ended capillary membranes|
|WO2005046847A1 *||Oct 17, 2003||May 26, 2005||Puron Ag||Method for producing a head piece comprising a fibre bundle consisting of open-ended capillary membranes|
|U.S. Classification||264/263, 210/321.9, 264/265, 385/143, 264/317, 264/DIG.440, 210/500.23|
|Cooperative Classification||Y10S264/44, B01D63/024, B01D63/022|
|European Classification||B01D63/02B10, B01D63/02D|